U.S. patent number 3,589,313 [Application Number 04/756,595] was granted by the patent office on 1971-06-29 for solid waste disposal method and apparatus.
Invention is credited to Dale A. Furlong, Ronald D. Kinsey, Richard D. Smith.
United States Patent |
3,589,313 |
Smith , et al. |
June 29, 1971 |
SOLID WASTE DISPOSAL METHOD AND APPARATUS
Abstract
A solid waste disposal system is described with a storage and
receiving carousel, a shredder, a dryer, a compressor-turbine
assembly for compressing air for combustion of waste and for
receiving hot gasses produced in the combustion process. Two
combustion systems, a fluid bed reactor and a gasifying pyrolyzer,
are described. Particulate matter harmful to the turbine and also
causing air pollution is removed from the hot high pressure gas
upstream of the turbine. The malodorous air from the waste storage,
shredding and drying is compressed and used for combustion and the
part of the hot exhaust gases from the turbine are used in the
dryer.
Inventors: |
Smith; Richard D. (Palo Alto,
CA), Furlong; Dale A. (Sunnyvale, CA), Kinsey; Ronald
D. (Cupertino, CA) |
Assignee: |
|
Family
ID: |
25044186 |
Appl.
No.: |
04/756,595 |
Filed: |
August 30, 1968 |
Current U.S.
Class: |
110/222; 55/343;
55/432; 55/459.1; 110/233; 55/315; 55/346; 55/447; 110/245 |
Current CPC
Class: |
F23G
5/46 (20130101); B03B 9/06 (20130101); F23G
5/30 (20130101); F23G 5/027 (20130101); F23G
2201/303 (20130101); F23G 2206/203 (20130101); F23G
2206/20 (20130101); F23G 2201/10 (20130101); F23G
2201/304 (20130101); Y02W 30/52 (20150501); F23J
2217/40 (20130101); Y02W 30/521 (20150501); F23G
2900/54601 (20130101); Y02E 20/12 (20130101); Y02W
30/527 (20150501); F23G 2201/80 (20130101); F23J
2217/102 (20130101); F23G 2201/40 (20130101); F23G
2202/30 (20130101) |
Current International
Class: |
F23G
5/30 (20060101); B03B 9/00 (20060101); F23G
5/46 (20060101); B03B 9/06 (20060101); F23G
5/027 (20060101); F23g 005/02 () |
Field of
Search: |
;110/7,8,29,28
;55/126,315 |
References Cited
[Referenced By]
U.S. Patent Documents
Primary Examiner: Favors; Edward G.
Claims
We claim:
1. Waste disposal apparatus comprising, in combination, a gas
turbine for compressing air and combusting substantially gaseous
material, a char combustion chamber, means for directing a portion
of the compressed air from said gas turbine to said char combustion
chamber, a pyrolyzing chamber, means for directing combustibles
into said pyrolyzing chamber, means for conveying char produced in
said pyrolyzing chamber into said char combustion chamber and for
directing inert gaseous products from said char combustion chamber
to said pyrolyzing chamber, and means for directing gaseous
products from said pyrolyzing chamber to said gas turbine for
combustion.
2. A waste disposal apparatus comprising, in combination, waste
storage means for receiving and storing solid waste; shredder means
for shredding the solid waste; dryer means for drying the shredded
waste; combustion means for burning the burnable portions of said
shredded dried waste at elevated pressure; means for conveying
solid waste from said storage means to said shredder means,
shredded waste from said shredder means to said dryer means, and
shredded dried waste from said dryer means to said combustion means
for combustion; a compressor-turbine assembly including means for
compressing and heating air for combustion of said waste; means for
directing said turbine compressed air to said combustion means;
means for drawing malodorous air into said gas turbine from said
dryer means, said shredder means and said storage means for
compression; said combustion means including a bed of inert
particles to which said shredded dried waste and said compressed
gases are directed for burning; means for collecting and removing
the unburnable portions of said waste from said combustion chamber;
means for removing the particles from the gaseous combustion stream
produced in said combustion means; means for directing the
combustion gases combustion gases from said combustion means to
said compressor-turbine assembly; means for expanding said
compressed hot gas in compressor-turbine assembly and means for
directing hot gas from said compressor-turbine assembly to said
dryer means.
3. The waste disposal apparatus of claim 2 including means for
generating power connected to and driven by said gas turbine.
4. The method of disposing of waste comprising the steps of
shredding the waste, drying the waste, mixing and burning the waste
with hot compressed air, expanding the burning exhaust to generate
shaft work to compress air and net shaft work, and drying other
waste with a portion of the expanded exhaust.
5. The method of consuming waste comprising the steps of shredding
the waste, drying the waste, compressing air, consuming the char
combustion products of the volatilization step with the compressed
air to produce hot inert gas and ash, volatilization of the waste
with hot inert gas to produce char combustion products and fuel
gas, burning the fuel gas in compressed air, and expanding the
exhaust to compress the air and provide shaft work.
6. A waste disposal apparatus of the type for consuming solid waste
refuse in a burner with minimal residue characterized by shredder
means for shredding solid waste material, dryer means for drying
the shredded waste, means for combusting portions of said shredded
refuse at elevated pressure and temperature, means for removal of
particulate matter from the hot high pressure gas which would be
injurious to a turbine or cause air pollution, means for conveying
solid waste from said shredder means to said dryer means and
shredded dried waste from said dryer means to said combustion
means, a compressor-turbine assembly for compressing intake gases
and directing the compressed gases to said combustion means, means
for directing gases heated by said combustion means to said
compressor-turbine assembly to drive said turbine, and means for
drawing into said compressor-turbine assembly malodorous air from
said shredder means, said dryer means, and said storage means as
intake gases for compression.
7. A waste disposal apparatus of the type for consuming solid waste
refuse in a burner with minimal residue characterized by shredder
means for shredding solid waste material, dryer means for drying
the shredded waste, means for combusting portions of said shredded
refuse at elevated pressure and temperature, means for removal of
particulate matter from the hot high pressure gas which would be
injurious to a turbine or cause air pollution, means for conveying
solid waste from said shredder means to said dryer means and
shredded dried waste from said dryer means to said combustion
means, a compressor-turbine assembly for compressing intake gases
and directing the compressed gases to said combustion means, means
for directing gases heated by said combustion means to said
compressor-turbine assembly to drive said turbine, and means for
directing hot exhaust gases from said turbine to said dryer means
for drying said waste.
8. A waste disposal apparatus of the type for consuming solid waste
refuse in a burner with minimal residue characterized by shredder
means for shredding solid waste material, dryer means for drying
the shredded waste, means for combusting portions of said shredded
refuse at elevated pressure and temperature, means for removal of
particular matter from the hot high pressure gas which would be
injurious to a turbine or cause air pollution means for conveying
solid waste from said shredder means to said dryer means and
shredded dried waste from said dryer means to said combustion
means, a compressor-turbine assembly for compressing intake gases
and directing the compressed gases to said combustion means, and
means for directing gases heated by said combustion means to said
compressor-turbine assembly to drive said turbine, said combustion
means including means for volatilizing at least portions of said
shredded dried waste and removing particulate matter from fuel gas
and including means for burning material volatilized in said
volatilizing means.
9. The waste disposal apparatus of claim 8 including a char
combustion chamber, means for feeding compressor-turbine assembly
compressed air into said char combustion chamber, means for
conveying char produced in said volatilizing means into said char
combustion chamber and for directing inert gaseous products from
said char combustion chamber to said volatilizing means.
10. A waste disposal apparatus of the type for consuming solid
waste refuse in a burner with minimal residue characterized by
shredder means for shredding solid waste material, dryer means for
drying the shredded waste, means for combusting portions of said
shredded refuse at elevated pressure and temperature, means for
removal of particulate matter from the hot high pressure gas which
would be injurious to a turbine or cause air pollution, means for
conveying solid waste from said shredder means to said dryer means
and shredded dried waste from said dryer means to said combustion
means, a compressor-turbine assembly for compressing intake gases
and directing the compressed gases to said combustion means, and
means for directing gases heated by said combustion means to said
compressor-turbine assembly to drive said turbine, said combustion
means including a char combustor chamber, means connected to said
compressor-turbine assembly and said char combustor chamber for
conducting compressed air from said compressor-turbine assembly to
said char combustor chamber, a pyrolyzer connected to said dryer
means via said conveying means for receiving said dried shredded
waste and connected to said char combustor chamber for combustion
and passing inert gaseous products from said char combustor chamber
to said pyrolyzer to volatilize dried shredded waste, and a gas
combustion chamber means connected to said pyrolyzer to receive and
burn volatilization materials produced in said pyrolyzer.
11. A waste disposal apparatus of the type for consuming solid
waste refuse in a burner with minimal residue characterized by
shredder means for shredding solid waste material, dryer means for
drying the shredded waste, means for combusting portions of said
shredded refuse at elevated pressure and temperature, means for
removal of particulate matter from the hot high pressure gas which
would be injurious to a turbine or cause air pollution, means for
conveying solid waste from said shredder means to said dryer means
and shredded dried waste from said dryer means to said combustion
means, a compressor-turbine assembly for compressing intake gases
and directing the compressed gases to said combustion means, means
for directing gases heated by said combustion means for directing
gases heated by said combustion means to said compressor-turbine
assembly to drive said turbine, and means connected to said
compressor-turbine assembly for establishing a partial vacuum and
refuse collection vacuum pipe means connected to said vacuum means
for conveying refuse to said storage and shredder means.
12. A waste disposal apparatus of the type for consuming solid
waste refuse in a burner with minimal residue characterized by
shredder means for shredding solid waste material, dryer means for
drying the shredded waste, means for combusting portions of said
shredded refuse at elevated pressure and temperature, means for
removal of particulate matter from the hot high pressure gas which
would be injurious to a turbine or cause air pollution, means for
conveying solid waste from said shredder means to said dryer means
and shredded dried waste from said dryer means to said combustion
means, a compressor-turbine assembly for compressing intake gases
and directing the compressed gases to said combustion means, means
for directing gases heated by said combustion means to said
compressor-turbine assembly to drive said turbine, and means
connected to the exhaust of said compressor-turbine assembly for
generating steam.
13. A waste disposal apparatus of the type for consuming solid
waste refuse in a burner with minimal residue characterized by
shredder means for shredding solid waste material, dryer means for
drying the shredded waste, means for combusting portions of said
shredded refuse at elevated pressure and temperature, means for
removal of particulate matter from the hot high pressure gas which
would be injurious to a turbine or cause air pollution, means for
conveying solid waste from said shredder means to said dryer means
and shredded dried waste from said dryer means to said combustion
means, a compressor-turbine assembly for compressing intake gases
and directing the compressed gases to said combustion means, means
for directing gases heated by said combustion means to said
compressor-turbine assembly to drive said turbine, and means for
directing sewage sludge into said combustion chamber assembly.
14. Waste disposal apparatus of the type for consuming solid waste
refuse in a burner with minimal residue and substantially
pollution-free gaseous output characterized by: a
compressor-turbine assembly including means receiving hot gases
produced in the combustion of such waste; means for shredding solid
waste material, combustion means for consuming most of the shredded
waste under elevated pressure and temperature including a bed of
incombustible inert particles, means for feeding compressor-turbine
assembly compressed air into said combustion chamber beneath said
particle bed, and means for feeding shredded waste from said
shredding means into said particle bed without additional fuel
whereby substantial portions of said waste are combusted in said
particle bed; means for removal of particulate matter from the hot
gases produced in said combustion means at substantially the
consuming elevated pressure and temperature; and means for
directing compressed and heated air from said compressor-turbine
assembly to said combustion means and hot gases from said
combustion and particle removal means to said compressor-turbine
assembly to drive said turbine; and means for directing at least
certain of the combustion gases from said turbine to
atmosphere.
15. Waste disposal apparatus of the type for consuming solid waste
refuse in a burner with minimal residue characterized by: a
compressor-turbine assembly including means for compressing air for
combusting waste material and means receiving hot gases produced in
the combustion of such waste; combustion means for consuming most
of the waste under elevated pressure and temperature including
means for volatilizing at least portions of said waste and means
for combusting material volatilized in said volatilizing means;
means for removal of particulate matter from the hot gases produced
in said combustion means at substantially the consuming elevated
pressure and temperature; means for directing compressed and heated
air from said compressor-turbine assembly to said combustion means
and hot gases from said combustion and particle removal means to
said compressor-turbine assembly to drive said turbine; and means
for directing waste into said combustion means.
16. The waste disposal apparatus of claim 15 including a char
combustion chamber to receive compressor-turbine assembly
compressed air and means for conveying char produced in said
volatilizing means into said char combustion chamber and for
directing inert gaseous products from said char combustion chamber
to said volatilizing means.
17. A waste disposal apparatus of the type for consuming solid
waste refuse in a burner with minimal residue and substantially
pollution-free gaseous output characterized by shredder means for
shredding solid waste material; dryer means for drying the shredded
waste; means for combusting portions of said shredded refuse at
elevated pressure and temperature including a combustion chamber
and a bed of inert particles positioned within said combustion
chamber, said particles being incombustible at the combustion
temperature of said shredded dried waste; means for removal of
particulate matter at substantially said elevated pressure and
temperature from the hot high pressure gas which would be injurious
to a turbine or cause air pollution; means for conveying solid
waste from said shredder means to said dryer means and shredded
dried waste from said dryer means to said particle bed without
additional fuel; a compressor-turbine assembly for compressing
intake gases and directing the compressed gases to said combustion
chamber beneath said particle bed; means for directing high
pressure exhaust gases heated by said combustion means to said
compressor-turbine assembly for expansion and drive of said
turbine; and means for exhausting at least certain of the
combustion gases from said turbine to atmosphere.
Description
The invention described herein was made in the course of or under a
contract with the Department of Health, Education and Welfare.
The present invention relates in general to a solid waste disposal
system and more particularly, to a combustion system wherein the
waste is consumed under pressure.
The disposal of solid waste (refuse) is one of the most critical
social problems today facing countries with large urban
populations. In the United States the urban areas where 67 percent
of the population lives produce 117 million tons of refuse a year,
an average of 5 pounds per person per day. City dumps, which have
historically been employed for economical refuse disposal, are
being closed because they are polluting the air.
Incineration of solid wastes is widely accepted as the most
desirable solution to the problem but has not been universally
adopted because of its high cost, particularly if the incinerator
meets air pollution standards. Sanitary land fills do not pollute
the air and are inexpensive, but sites adjacent to urban areas are
filling up and suitable new sites are not generally available.
The object of the present invention is to provide an economical
solid waste disposal method and apparatus acceptable for urban
use.
Broadly stated, the present invention, to be described in greater
detail below, is directed to a solid waste disposal system
including a compressor-turbine assembly which operates to compress
air for combusting waste material and for receiving hot gases
produced in the combustion of such waste, means for combusting the
combustible portions of the waste, means for directing the
compressed and heated air from the compressor-turbine assembly to
the combustion chamber assembly and hot gases from the combustion
chamber assembly to the compressor-turbine assembly to drive the
turbine, and means for directing waste into the combustion chamber
assembly.
One feature and advantage of the present invention lies in the fact
that the energy of the refuse extracted by combustion is utilized
to operate the waste disposal system. A solid waste disposal system
can be provided efficiently to consume the refuse from a community
of 160,000 residents. Additionally, by combusting the waste under
pressure, greater efficiency is achieved and a smaller facility can
be utilized. In the burning chamber, the elevated pressure
increases the amount of available oxygen and also increases the
heat transfer from the hot gases to the solid waste.
In accordance with another aspect of this invention, a generator,
such as an electric generator, is connected to and driven by the
compressor-turbine assembly so that power can be generated from
refuse energy and provided to the community responsible for the
waste which serves as the fuel to drive the generator. Thus, the
disposal plant can provide five to ten percent of the electric
power requirements of the community generating the waste handled by
the plant. Besides a direct return to the community to effectively
reduce the cost of waste disposal this system conserves the natural
resources.
In accordance with still another aspect of the present invention,
the combustion means for the disposal system is a particle fluid
bed reactor. The fluid bed provides heat transfer rates from the
bed to the incoming solid waste approximately 5 to 10 times greater
than conventional grate burners and at the same time provides a
scrubbing action between the bed and the waste to continuously
remove char from the burning surface of a solid thereby exposing
virgin material to the oxygen environment for combustion. Still
further, the fluid bed reactor provides a highly uniform
temperature throughout eliminating regions of high local
temperature where undesirable nitrogen-oxygen compounds would be
formed.
In accordance with still another aspect of the present invention,
combustion of the solid waste is accomplished by volatilization and
subsequent burning of the volatilized fuel gas in a conventional
gas turbine combustion chamber which is a part of the
compressor-turbine assembly. In accordance with this aspect of the
present invention, the solid waste is directed to a pyrolyzing
chamber and there subjected to hot inert gases for pyrolysis and
vaporization of volatile combustible material. From the pyrolyzing
chamber, volatilized fuel gas is conducted to the combustion
chambers of the compressor-turbine assembly and the remaining char
is conducted to a char combustion chamber. A portion of the
compressed air from the compressor of the compressor-turbine
assembly is fed to the char combustor to burn the char and produce
hot inert gas that is carried to the pyrolyzing chamber.
With the gasifier system in place of the fluid bed reactor, the
particle collection problem from the stream of burned material is
eased because only a small percentage of the total air flow of the
gas turbine passes through the combustor. Furthermore, the gas
turbine combustors normally supplied can be used to burn the hot
gases with no alterations to the compressor-turbine assembly
required to conduct the air away from the compressor, or the hot
gas to the turbine.
In accordance with still another aspect of the present invention,
the waste material is first shredded and then dried before
combustion utilizing part of the hot exhaust gases from the gas
turbine in the drying step. This feature of the present invention
not only increases the efficiency of the waste disposal method and
apparatus by increasing the burning rate and eliminating
operational variations due to different moisture contents but also
accomplishes the drying function with heat that is a byproduct of
the system.
As still another aspect of the present invention the malodorous air
from the refuse storage, shredding and drying area is drawn into
the turbine air compressor so that the waste disposal plant does
not create an undesirable smell and is acceptable for placement in
an urban area.
In accordance with still another embodiment of the present
invention the compressor-turbine assembly is used as a vacuum pump
to pull refuse through vacuum lines into the waste disposal system
to serve as the waste collection means.
In accordance with still another aspect of the present invention,
particle separators are provided for the combustion chamber
assembly to remove particulate matter harmful to the turbine. The
particle separators can be inertial separators, electrostatic
precipitators and/or mat filters. In one embodiment of this
invention, the particle separator assembly includes an inertial
separator followed by an electrostatic precipitator. The inertial
separator removes all but the smallest particles and these small
particles are removed by the electrostatic precipitators.
A feature and advantage of the particle separation utilized in the
present invention lies in the fact that removal of the particles
upstream of the turbine not only prevents damage to the turbine but
also removes the particles that would cause air pollution.
In accordance with still another aspect of the present invention, a
multistage flash evaporator system or equivalent system can be
added to the solid waste disposal system to provide 2,500,000
gal/day of fresh water from sea water or 20 to 30 percent of the
water required by 160,000 people. The waste heat from the hot gases
downstream of the turbine are used to provide the energy for the
evaporator systems.
In accordance with still another aspect of the present invention, a
sewage sludge disposal system can be provided by the waste disposal
system aforementioned for burning the sewage sludge residue from a
sewage plant handling the sewage from the same 160,000 people
served by the solid waste disposal plant.
These and other features and advantages will become more apparent
upon a perusal of the following specification taken in conjunction
with the accompanying drawings wherein similar characters of
reference refer to similar structures in each of the several
views.
In the drawings:
FIG. 1 is a schematic flow diagram of a waste disposal system and
illustrates the operation of several different aspects of the
present invention.
FIG. 2 is a schematic diagram illustrating different system
utilizations for the present invention.
FIG. 3 is a plan view of an operative embodiment of the present
invention.
FIG. 4 is an elevational view, partially in section, of the
embodiment illustrated in FIG. 3.
FIG. 5 is an elevational schematic view of a fluid bed reactor
operable with the present invention.
FIG. 6 is a schematic block diagrammatic view of an alternative
fluid bed reactor system in accordance with the present
invention.
FIG. 7 is a schematic block diagram of a gasification system
utilized with the present invention.
FIG. 8 is an elevational sectional view through an operative
embodiment of a gasifier system in accordance with the present
invention.
FIGS. 9 and 10 are elevational schematic views illustrating
alternative gasifier systems utilizable with the present
invention.
Referring now to the drawing, with particular reference to FIG. 1,
there is shown an illustrative embodiment of the present invention.
As schematically illustrated, the method and apparatus of the
present invention are practiced utilizing a waste receiving and
storage assembly A, a shredding assembly B, a drying assembly C, a
compressor-turbine assembly D, a combustion chamber assembly E, and
an electric generator assembly F.
The solid wastes are typically received in accordance with one
embodiment of the present invention from municipal collection
trucks 10 which dump the waste into the receiving and storage
assembly A which includes a circular turntable or carousel 11
floating on a pond of water 13 within a hollow cylindrical housing
12 with suspended glass cloth panels 14 permitting truck access to
the carousel and with the carousel rotatable to feed the solid
wastes W into the shredding assembly B. The carousel 11 can be
raised and lowered to assist refuse dumping and feeding operations
by adjusting the level of pond 13 thereby eliminating the need for
a crane and associated high-bay construction in the solid waste
storage area. A large effective tipping area for the collection
trucks 10 is provided by the circular shape of the carousel 11 and
the panels 14 screen off the storage area while permitting an
inflow of fresh air.
The solid wastes W are directed by a fixed leveling blade 15 over
the carousel 11 into conveyors or a chute 16. The turntable
elevation and the rotational speed can be controlled automatically
or remotely controlled by an operator in the central control room
of the waste disposal plant where the operator observes the
carousel operation by closed circuit television.
In the shredding assembly B, all of the solid wastes W are shredded
to form a more nearly homogenous shredded material W.sub.s which is
easily transported through the remainder of the system by
conventional automated devices for materials handling. While
various solid waste constituents, such as magnetic material, can be
separated at this stage of operation, such as by magnetic
separators, such separation assemblies unduly increase the cost of
the system, and if separated at this stage, noncombustible would be
contaminated and would require special handling. Since shredders
are high maintenance items compared to the other subassemblies of
the operating system, two shredder assemblies are utilized in the
operating embodiment of the invention illustrated in FIG. 3 so that
an operational standby unit is available in the event of
failure.
The shredded solid wastes W.sub.s are dried in the drying assembly
C to increase the burning rate of waste in the overall system and
eliminate the variability in burning rate resulting from widely
different moisture contents. A rapid and uniform burning rate
promotes clean combustion and reduces the required size of the
combustion chamber to be described below. In the embodiment
illustrated in the drawings the drying assembly C includes a hollow
cylindrical rotating dryer 17 which produces considerably mixing
and blending during the drying step to offset any local
concentration of one constituent of solid waste.
In accordance with one aspect of the present invention, the heat
utilized in the drying assembly C is provided by a heated air
stream 18 which obtains its heat from a portion of the exhaust
gases 19 from the gas turbine assembly D.
The compressor-turbine assembly draws at least a portion of its
compressor intake air 21 through a filter 22 from the air space
above the waste in the receiving and storing, shredding and drying
assemblies, A, B, and C, respectively, to prevent dust and odors
from escaping to the environment. All of the malodorous gases
carried on into the compressor portion 20 of the gas turbine
assembly D are subsequently subjected to elevated temperatures and
sterilization before release. The shredded and dried solid waste
W.sub.sd is transported via a conduit 23 and fed into the high
pressure environment of the combustion chamber assembly E such as
by a rotary feeder 24. The speed of the rotary feeder is adjusted
by a control system to maintain proper temperature and gas flow
within the disintegration assembly E.
In the compression portion 20 thereof the compressor-turbine
assembly D compresses the intake air 21 from the other assemblies
and from the outside environment to elevated pressures and
temperatures such as 100 p.s.i.a. and 584.degree. F. or 200
p.s.i.a. and 700.degree. F. This hot high pressure air is ducted
via conduit 25 to the combustion chamber assembly E to provide the
oxygen for combustion of the solid wastes.
The combustion chamber assembly illustrated in FIG. 1 and in
enlarged scale in FIG. 5 includes a combustion chamber 31 in the
form of a fluid bed reactor. Sand or other inert particles 32 are
contained within the chamber 37 above a porous grate 33 and
suspended or fluidized during operation by passing air
therethrough. Limestone or dolomite can be added to the particle
bed for control of noxious gases. The shredded dried waste W.sub.sd
is injected directly into the bed of particles 32 by a conduit 34
from the rotary feeder 24. This bed of particles 32 is initially
heated by an external source (not shown) to an elevated temperature
for combustion of waste material and combustion is maintained with
the compressed hot gases from the compressor-turbine assembly D
passing into combustion chamber 31 from conduit 25 and through the
grate 33.
The fluidized bed promotes dispersion of the incoming shredded and
dried solid waste which is heated to ignition temperature and
maintained in the bed a sufficient time for combustion of all
burnable solid waste particles. The particles are selected within
suitable range of size, shape and density and of a material to
withstand high temperatures without slagging and the air is caused
to flow through the particles under carefully controlled
conditions. Chief among these conditions is the necessity that the
fluid velocity through the bed, and hence the pressure drop, be
greater than the value required to support the bed weight but less
than the value required to sweep the particles out of the chamber.
When these conditions are satisfied, the bed particles exist in a
fluidized state. If the movement of one specific particle could be
observed, it would undergo a continuous turbulent motion, being
bouyed by flowing fluid and not at rest against adjacent particles.
Superimposed upon this localized motion are convection motions of
the entire bed. Viewed as a whole, the dynamic condition of a
fluidized bed is quite analogous to that of a boiling liquid.
The high pressure and turbulence in the fluid bed reactor combine
to promote rapid combustion of the solid wastes. Thus, the
fluidized inert material promotes dispersion of the incoming
shredded solids, heats the solid waste to ignition temperature, and
maintains residence time sufficient for combustion of all burnable
solid waste particles within the reactor. The fluid bed will hold a
kleenex long enough for it to be burned without escaping while at
the same time heave chunks heavy rubber will remain in the bed
until finally consumed. Large pieces of inert material will sink to
the bottom of the bed and be removed from the fluid bed through an
air lock feeder 35 and combined with other ash in a residue storage
35'.
The burning rate of this combustion chamber assembly in accordance
with the present invention is greatly increased over the burning
rate of conventional assemblies by reason of the increased pressure
for availability of additional oxygen, increased heat transfer to
the solid waste by the radiation from the large surface area of the
particulate matter and convective heat transfer from the hot gas,
the large direct surface area of the waste due to shredding, the
continual abrasion of the charred surface by the bed material to
expose virgin waste surface, and the continual mixing of gases in
the bed enhancing the flow of gases to and from the burning solid
surface thereby enhancing the completeness and rate of gas phase
combustion reaction.
Most of the ash remaining after combustion is complete will be
carried off with the gases leaving the fluid bed surface and
subsequently collected by particle collectors 36. The ash particles
and inerts from the solid waste which are larger or more dense than
the inert particles 32 forming the bed eventually reach the bottom
of the fluid bed reactor in the combustion chamber where they are
removed by the rotary air lock 35.
In addition to the advantages of the high pressure fluid bed
combustor mentioned above, the highly uniform temperature, the
presence of CaO and MgO in the ash, or the addition of limestone or
dolomite, greatly reduce the air pollution from burning of solid
wastes. The thorough mixing of the fluid bed maintains a highly
uniform temperature so that few nitrogen-oxygen compounds, formed
when nitrogen and oxygen gases are exposed to elevated
temperatures, are formed. The CaO and MgO in the ash or limestone
or dolomite suppresses evolution of sulfur dioxide and other acid
vapors by chemically combining with the acids to form a salt.
Although solid waste has a relatively low sulfur content (0.1
percent) compared to petroleum or bituminous fuels, it contains
polyvinylchloride plastic which evolves hydrochloric acid vapor
when burned. The fluid bed combustor is ideally suited to the
efficient utilization of the natural properties of the ash or of
limestone or other suppressant because this material would be
retained in the bed and the chemical reactant continuously removed
from the suppressant by the fluid bed turbulence.
The hot gases leaving the fluid bed 32 entrain many ash particles
which must be removed such as by the particle collectors 36 before
the gases are allowed to enter the turbine. Large particulate
matter, if allowed to pass through the turbine, will damage the
turbine severely. Gas cleaning by the particle collectors 36 and
accomplished for the turbine also satisfies the clean air
requirements for exhaust gases. The particle collectors can take a
number of different forms such as inertial separators,
electrostatic precipitators and mat filters. The particle
collectors 36 in FIGS. 1 and 5 are schematically illustrated as a
combination of inertial separators 42 followed by electrostatic
precipitators 43. The inertial separators 42 remove all but the
smallest particles, and these small particles are removed by the
electrostatic precipitators 43.
Inertial separators use centrifugal force to separate particles
from the gas stream and can provide efficiencies of 97.8 percent
and greater for particles as small as 10 microns in diameter, but
the efficiency degrades for particles smaller than this size. The
fine particles which tend to follow the air flow out of inertial
separators are least likely to injure the turbine. Inertial
separators are particularly suited for use in the first stage of a
two stage separator because they efficiently remove large
particles, leaving only the fines for the second stage.
Electrostatic precipitators directly charge the particles in the
gas and subsequently attract them to a surface charged with
opposite polarity. Since the forces of separation are applied
directly to the particles without disturbing the gas flow, all
sizes of particles are collected efficiently; however, the high
collection efficiency for the fine particles (5 microns and below)
is particularly good. As temperature is increased in an
electrostatic precipitator, the electrical characteristics of the
hot has change due to molecular action, and it becomes more
difficult to charge the dust particles. Fortunately, increased
pressure as utilized in the air chamber of the present invention
tends to offset this characteristic. Mat filters have excellent
collection efficiency for both coarse and fine particles and filter
material is available made of fine fibers (5 to 7 microns in
diameter) of silicon dioxide and aluminum oxide which can be used
as filter material up to 2300.degree. F.
The hot gases leaving the particle collectors 36 are expanded
through the expansion and drive portion 37 of the
compressor-turbine assembly D which drives the compressor portion
20 of the assembly D, and drives the electric generator assembly F
to produce electric power.
The hot has leaving the compressor turbine assembly D is near
atmospheric pressure but at elevated temperature so that the
portion 19 can be utilized for drying shredded solid waste material
in the drying assembly C as described above. If solid waste has a
moisture content of 20 percent and this moisture is boiled out in
the dryer, less than 10 percent of the exhaust gases need be
recirculated. An optional exhaust heat recovery boiler 38 can be
provided in the exhaust line from the gas turbine for utilization
of the heat for producing steam for heating, air conditioning, or
desalting water. The hot exhaust gas is decelerated in an enlarged
exhaust plenum and released to the atmosphere from a large area in
the roof of the plant.
As illustrated in FIG. 2, use of the gas turbine cycle for waste
collection allows performance of many services to the community
besides incineration of solid wastes. For example, the capability
of the gas turbine compressor can be utilized to draw a powerful
vacuum and suck the solid waste through underground pipes and
deposit this waste in the carousel for combustion in the disposal
system. Alternatively, the exhaust heat from the gas turbine can be
utilized to produce fresh water daily from saline or brackish
water. Still further, the disposal system can be utilized to
incinerate the sewage sludge resultant from sewage systems.
In the modern field of power generating equipment, the gas turbine
is most suited for the capacity range of 5 to 30 megawatts, above
diesel and gas engine generators for lower powers and below steam
turbine generators for higher powers. The present invention is
specifically designed for providing as an advanced incinerator a
compact module consuming between 200 and 800 tons per day and
generating through an electric generator between 7 megawatts and 30
megawatts of electric power. By way of example, several gas
turbines are presently available in the 15 megawatt capacity and
correspond to a solid waste disposal capacity of 400 tons per day,
approximately in the middle range of interest. A 400 ton per day
unit will dispose of solid wastes from approximately 150,000
people; for their entire population San Francisco would require 5
units of this size, New York would require 40 units. Such a unit
will dispose of solid waste for 95 per ton, approximately one-half
the cost of sanitary land fill and 16 percent the cost of modern
conventional incinerators. Additionally, such a unit can supply 5
to 10 percent of the electric power requirements of the community
serviced by the incinerator. By using a carousel storage volume 15
feet deep with an inside diameter of 80 feet, 2,790 cubic yards of
solid waste can be stored which supports over 26 hours of
continuous operation of the 400 ton per day disposal unit. Also,
such a 400 ton per day unit will operate with two fluid bed
reactors (plus a spare for emergencies) each operable with a
maximum air flow of 100 pounds per second and solid waste feed rate
of 200 tons per day. Typical reactors can have a diameter of 10
feet, a reactor bed depth of 3 feet, an average air velocity of 12
feet per second and a reactor pressure drop of 6 p.s.i. Such
reactors have a heat release rate of 500,000 B.t.u. per hour for
each cubic foot of fluid bed and a heat release rate of 1,000,000
B.t.u. per hour per square foot of area.
In accordance with another aspect of the present invention, an
alternate configuration for the fluid bed reactor as shown in FIG.
6 is provided. In this arrangement, the compressor air from the
compressor portion of the compressor-turbine assembly D is heated
by passing through pipes 39 immersed in the fluid bed 32' with the
heated air from these pipes then expanded through the expansion and
drive portion 37 of the compressor-turbine. Since the combustion
process takes place outside these pipes 39 rather than directly in
the gas that passes through the turbine, the process of this aspect
of the present invention can be considered as external combustion.
Air 41 is supplied to the external fluid bed reactor 32' by a
forced draft fan (not shown). Only enough excess air 41 is supplied
to insure complete combustion, and thus the weight flow rate of air
passing through the fluid bed reactor is approximately one-fifth
that passing through the gas turbine. To minimize the heat transfer
area, the bed is operated as hot as possible such as 1900.degree.
F. without slagging the ash. Since the combustion gases do not pass
through the gas turbine, they may be cooled prior to particle
collection.
An external fluid bed reactor constructed in accordance with this
embodiment of the present invention can provide a solid waste
disposed rate of about 250 tons per day with an average air
velocity of 5 feet per second in a bed area and volume of 3880
ft..sup.2 and 930 ft..sup.3 respectively, with a heat release of
over 100,000 B.t.u. per cubic foot utilizing a forced draft fan
power of 610 horsepower.
The combustion of hydrocarbon materials principally found in solid
waste occurs in three distinct phases and these phases occur almost
independently in all combustion processes. In the first phase,
called pyrolysis or volatilization, the material is heated, causing
decomposition of the hydrocarbon solids into hydrocarbon gases;
next these gases are oxidized in a gas phase reaction; and finally,
the solid carbonaceous char remaining after volatilization is
oxidized.
In accordance with still another aspect of the present invention,
the combustion of the waste material can be accomplished in
cooperation with the gas turbine by a gasification method and
apparatus as illustrated in FIGS. 7--10 taking advantage of the
distinctions between these phases.
In the gasifier concept of the present invention, each of these
phases occurs in a separate location. The shredded and dried solid
waste material W.sub.sd is first injected into a pyrolyzer or
pyrolyzing chamber 51 from a conduit 50 where the first phase
pyrolysis or volatilization takes place. The combustible
hydrocarbon gases generated in the pyrolyzing chamber 51 serve as a
gaseous fuel for the gas turbine where the gas phase oxidation
occurs in the gas turbine combustors 53. Hot inert gases are also
injected into the pyrolyzer for pyrolyzation of the solid wastes.
These hot inert gases are separately generated in a char combustion
chamber 52 which for the third phase oxidizes the residual solid
char coming from the pyrolyzer with air bled from the compressor
portion 19' of the gas turbine assembly D'. The bleed air that is
directed into the char combustion chamber 52 from the gas turbine
compressor is compressed in a supercharger 54 (approximately 5
percent of the gas turbine flow rate) to account for pressure
losses in both the char combustor chamber 52 and the pyrolyzing
chamber 51.
The purpose of the pyrolyzer is to chemically decompose, or
pyrolyze, the incoming solid wastes. Pyrolysis is accomplished by
heating in an oxygen-free environment and the necessary heat is
derived from hot inert gases (over 3000.degree. F.) supplied to the
pyrolyzer 51 from the char combustor 52. In one embodiment of the
gasifier system illustrated in FIG. 8, the pyrolyzer 51 includes a
fluid bed reactor of inert particles 55 similar to but smaller than
the fluid bed reactor described above with reference to FIGS. 5 and
6 and wherein the particle bed is supported on a downwardly
directed conical, porous injector plate 56 apertured at the conical
apex. Abrasion by the fluid bed will rapidly remove char as it is
formed on the surface of waste material and this fine char material
thus abraded will be carried out of the fluid bed by gases and
subsequently separated by particle collectors 36".
The primary constituent of the organic fraction of the solid waste
material is cellulose, the chief component of all wood and plant
fibers, and hence of all paper products. In the fluid bed 55 in the
pyrolyzing chamber 51, degradation of the cellulose material will
occur and eventually all the oxygen and hydrogen, and a substantial
part of the carbon, will be driven off leaving a carbonaceous char
and nondecombustible ingredients such as metal and glass. Most of
the carbon driven off is in the form of fine particles produced by
the abrading action of the particle bed. Oxidation of this fixed
carbon particulate in the pyrolyzer 51 could not be accomplished
without burning some of the fuel gases. Therefore, in accordance
with this aspect of the present invention, this char particulate is
removed from the pyrolyzer and returned via a conduit 58 to the
char combustor 51 where it is burned at near stoichiometric fuel
air ratios for generation of the inert gases for the pyrolyzer
51.
One construction for the char combustor 52 in accordance with the
present invention and as illustrated in FIG. 8, is a vortex
combustor consisting of a cylindrical housing 57 with a ceramic
lining and into which compressor air with entrained fine char
particles recovered from the pyrolyzer gases by the particle
collectors 36" via conduit 58 is introduced tangentially via a
conduit 59 at high velocity such as 300 feet per second causing
gases in the combustor chamber 52 to flow in free vortex motion.
Centrifugal force causes solid particles entrained in the vortex to
continue to rotate until consumed or slowed by contact with the
walls while the inert gases increase in angular velocity and are
removed from the core of the vortex and pass through a reentrant
throat section 61 and the ceramic injector plate 56 into the fluid
bed pyrolzyer 51. Since the temperature in the combustor is above
3000.degree. F., the ash and metals are melted and these molten
droplets collect on the wall of the chamber. Larger particles stick
to the molten ash and are exposed to a relatively high velocity air
stream promoting rapid combustion. The liquid ash and metal
subsequently drain through a hole 62 in the bottom of the char
combustor 52 into a quench tank 63. There the molten residue is
suddenly quenched in water resulting in the formation of granular
residue which is removed as a water slurry.
As described above the hot inert gases from the combustor 52
fluidize the particle bed 55 and volatilize combustibles therein.
Large pieces of solid waste that are not buoyed up by the fluid bed
55 migrate to the apex of the conical injector 56. There, these
pieces are continuously exposed to the entering 3000.degree. F. gas
stream from the combustor 52 and rapidly are either pyrolyzed or
melted. If melted, the molten residue drips directly into the
quench tank 63 through the core of the vortex combustor chamber
57.
An integrated gasifier in accordance with this construction
approximately 4 feet in diameter and 20 feet high will process 200
tons of solid waste material in 24 hours.
The high temperature of the fuel gas going from the pyrolyzer 51 to
the gas turbine combustors 53 will assist rapid, complete
combustion, and since only this high temperature gaseous fuel is
combusted, it becomes unneccessary to use a high core temperature
combustor thereby avoiding generation of the usual nitrogen oxides
and promoting uniform temperature profile in the combustor.
The gasifier combustion method and apparatus of FIGS. 7 and 8
operates exceptionally well to avoid air pollution. For example,
SO.sub.2 and HC1 are removed in the fluid bed pyrolyzer 51 by
reaction with basic ash materials such as CaO and MgO. Limestone or
dolomite can be added to the pyrolyzer bed to aid this reaction,
however, in most cases sufficient CaO and MgO already exist in the
solid waste ash. Furthermore, nitrogen-oxygen compounds will not be
generated in the pyrolyzer chamber 51 since practically no oxygen
is present.
For a 400 ton per day capacity waste disposal plant of the type
described in FIGS. 7 and 8 existing gas turbines such as the
General Electric G5191 heavy duty industrial gas turbine or the
Pratt & Whitney ST4A-8 gas turbine can be utilized with only
minor modification.
Other combustion methods and apparatus besides the fluid bed
reactor described with reference to FIGS. 5 and 6 and the gasifier
described with reference to FIGS. 7 and 8, can be utilized with the
present invention.
By way of example, a simple gravity feed gasifier schematically
illustrated in FIG. 9 can be utilized. In this construction, solid
wastes are introduced at the top of a volatilizing chamber and fed
by gravity as they are volatilized and burned to ash, which is
removed continuously from the bottom. Air is directed up through
the gasifier 70 after being introduced into the ash region and the
air velocities are low to preclude agitation of the pyrolyzing
products. After passing through the ash, the air reaches the carbon
combustion zone where the carbon is combined with a limited supply
of oxygen to form carbon monoxide. Water is also introduced and the
resultant steam and hot carbon result in the "producer gas"
reaction which yields hydrogen and carbon monoxide and absorbs
heat. The flow rates of water and air are controlled such that all
the carbon is consumed, while assuring that slagging temperatures
are not reached. The hot gases rising from the carbon combustion
zone furnish heat to pyrolyze or volatilize the incoming solid
waste, thereby generating the fuel gas which is ducted into the gas
turbine combustors for final combustion with the primary air flow
coming from the turbine compressor.
Another combustion method and apparatus is schematically
illustrated in FIG. 10 and consists of a dual fluid bed gasifier
80. In the dual bed the oxygen necessary to combust the carbon is
separated from the initial pyrolysis process. Solid wastes are
introduced into the upper or volatilizing fluid bed where they are
pyrolyzed by hot inert gases coming from the carbon combustion
fluid bed. Rapid, uniform pyrolysis is assured by the highly
stirred conditions existing in the fluid bed. The fuel gas
resulting from the pyrolysis passes through particle collectors on
its way to the gas turbine combustor. The particles collected
contain both ash and carbonaceous char generated by the pyrolysis
process. This char is burned by introducing the particles into the
second or carbon combustion fluid bed and fine ash is separated
from the second bed affluent by a second set of particle
collectors. Ash slagging temperatures are prevented in the carbon
bed by limiting the available oxygen and by introducing water or
steam.
With the present invention still other combustion chamber
assemblies could be used such as a horizontal vortex combustor, a
vertical vortex combustor or a more conventional grate burner.
Although the foregoing invention has been described in some detail
by way of illustration and example for purposes of clarity of
understanding, it is understood that certain changes and
modifications may be practiced within the spirit of the invention
as limited only by the scope of the appended claims.
* * * * *